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Waste processing system and fuel reformer used in the waste processing system

Inactive Publication Date: 2000-01-18
HITACHI LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

A first objective of the present invention is to provide a waste-to-energy incineration system which is able to stably decompose generated dioxin, in which the composition and the heat value of exhaust gas fluctuates over time, and which utilizes a fuel reformer used there.
A second objective of the present invention is to provide a waste-to-energy incineration system and a fuel reformer which are able to stably decompose generated dioxin and to suppress NOx generation.
A second objective of the present invention is to provide a waste-to-energy incineration system having a highly reliable performance with respect to dioxin decomposition and a highly efficient waste-to-energy incineration performance.

Problems solved by technology

Since the previously-mentioned indirect heat exchange type fuel reformer includes a burner for heating a reaction tube, such a fuel reformer has a problem in that the size of the apparatus becomes large, and an external heat source has to be provided.
In particular, removal of dioxin has been a very pressing subject.
Further, since various kinds of waste are burned in an incinerator, the amount of generated heat changes hour by hour, month by month and year by year.
Consequently, since the amount of fuel fed to a fuel reformer changes, corresponding to the amount and the components of gas exhausted from the incinerator, an existing direct heat exchange type fuel reformer has a problem, that, a fire-proofing brick structure part inside the incinerator is easily damaged and worn out due to the changes of the generated heat.

Method used

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  • Waste processing system and fuel reformer used in the waste processing system
  • Waste processing system and fuel reformer used in the waste processing system
  • Waste processing system and fuel reformer used in the waste processing system

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Embodiment Construction

At first, details of the present invention will be explained with reference to an embodiment shown in FIGS. 1-4. FIG. 1 is a system diagram of a waste-to-energy incineration system of an embodiment according to the present invention, and FIG. 2 is a vertical sectional view of a fuel reformer of the embodiment of FIG. 1. In each of FIG. 3 and FIG. 5, variations of the waste-to-energy incineration system shown in FIG. 1, are shown.

As shown in FIG. 1, the waste-to-energy incineration system is divided into two main systems, that is, a steam turbine system and an exhaust gas system including a fuel reformer. In an incinerator 19, a part for storing waste 16 is provided, and air is injected into the incinerator 19 through the part for storing waste 16 by a compressor fan 17. The air injected into the incinerator 19 is used as waste burning air. The burned waste gas 20 generated in the incinerator is sent to a dust collector 26 via an exhaust gas pipe 24 after flowing through an incinerat...

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Abstract

A waste-to-energy incineration system, in which the amount and heat value of exhaust gas largely changes in long and short periods, comprises an incinerator for burning waste, a boiler in the incinerator for generating steam with exhaust heat generated by the incinerator, a superheater for superheating steam generated in the boiler, a steam turbine driven by steam superheated by the superheater, a generator driven by the steam turbine, a fuel reformer for reforming source fuel, and a combustor burning fuel gas reformed by the fuel reformer and at least a part of exhaust gas led from the incinerator which is able to stably decompose generated dioxin in waste incineration exhaust gas.

Description

1. Field of the InventionThe present invention relates to a fuel reformer, and a waste processing system including reformer, especially to a direct heat exchange type, non-catalyst fuel reformer, and a waste-to-energy incineration system in which a direct heat exchange type, non-catalyst fuel reformer is adopted.2. Description of Related ArtAs a fuel reformer for reforming source fuel such as hydrocarbon material to a gas containing hydrogen, an indirect heat exchange type fuel reformer or a direct heat exchange type reformer has been largely used. Further, there are two types of fuel reformers, that is, a fuel reformer using a catalyst and a fuel reformer which does not use a catalyst.In an indirect heat exchange type fuel reformer, a reaction tube and a burner are provided. While the reaction tube is heated by the combustion gas from the burner, raw gas enters the reaction tune at an end of the reaction tube. Further, the raw gas is partially oxidized (so-called partial combustion...

Claims

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Application Information

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IPC IPC(8): B01B1/00C01B3/00C01B3/36C01B3/38F01K3/00F01K3/24F23G5/027F23G5/46F23J15/08F01D15/10F01K27/02F02C7/22F22G1/16
CPCB01B1/005C01B3/36C01B3/38F01K3/247F23G5/0276F23G5/46F23J15/08F23G2202/106F23G2206/10Y02E20/12Y02P20/129
Inventor OKUSAWA, TSUTOMUKOYAMA, KAZUHITOYAMAGISHI, MASAHIKOHATAMIYA, SHIGEOAJIRO, TAIKOSUNOU, MEGUMIISHIGAKI, YUKIO
Owner HITACHI LTD
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